US4882064A - Method of removing impurities from hard waters or waters with significant calcium/magnesium concentrations - Google Patents
Method of removing impurities from hard waters or waters with significant calcium/magnesium concentrations Download PDFInfo
- Publication number
- US4882064A US4882064A US07/065,153 US6515387A US4882064A US 4882064 A US4882064 A US 4882064A US 6515387 A US6515387 A US 6515387A US 4882064 A US4882064 A US 4882064A
- Authority
- US
- United States
- Prior art keywords
- coagulant
- water
- adsorbent
- softened
- washing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims abstract description 31
- 239000012535 impurity Substances 0.000 title claims abstract description 8
- 239000011575 calcium Substances 0.000 title claims description 24
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 title claims description 17
- 239000011777 magnesium Substances 0.000 title claims description 8
- 239000003643 water by type Substances 0.000 title description 4
- 229910052791 calcium Inorganic materials 0.000 title description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title description 2
- 229910052749 magnesium Inorganic materials 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 82
- 239000000701 coagulant Substances 0.000 claims abstract description 60
- 239000003463 adsorbent Substances 0.000 claims abstract description 53
- 239000002245 particle Substances 0.000 claims abstract description 20
- 238000001179 sorption measurement Methods 0.000 claims abstract description 16
- 239000002344 surface layer Substances 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims abstract description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 7
- 239000011707 mineral Substances 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 6
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 34
- 229910001424 calcium ion Inorganic materials 0.000 claims description 31
- 229910001425 magnesium ion Inorganic materials 0.000 claims description 31
- 238000005406 washing Methods 0.000 claims description 21
- 238000005352 clarification Methods 0.000 claims description 20
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 claims description 18
- 239000003513 alkali Substances 0.000 claims description 10
- 239000000243 solution Substances 0.000 claims description 10
- 229920000867 polyelectrolyte Polymers 0.000 claims description 9
- 239000003929 acidic solution Substances 0.000 claims description 8
- 239000012670 alkaline solution Substances 0.000 claims description 7
- 239000008233 hard water Substances 0.000 claims description 7
- 230000001172 regenerating effect Effects 0.000 claims description 2
- 239000002250 absorbent Substances 0.000 claims 8
- 230000002745 absorbent Effects 0.000 claims 8
- 238000004064 recycling Methods 0.000 claims 3
- 238000010521 absorption reaction Methods 0.000 claims 1
- 238000011069 regeneration method Methods 0.000 description 27
- 230000008929 regeneration Effects 0.000 description 26
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 16
- -1 Mg2+ ions Chemical class 0.000 description 13
- 238000012360 testing method Methods 0.000 description 9
- 239000002253 acid Substances 0.000 description 6
- 238000003795 desorption Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003922 charged colloid Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000012492 regenerant Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
Definitions
- This invention relates to improvements in processes for water clarification.
- the invention is concerned with improvements and modifications of the water clarification processes described in our Australian Pat. No. 512,553 and patent application No. 40032/78.
- a "coagulant/adsorbent” consisting of a finely-divided particulate material, the individual particles of which have been treated to produce a thin hydroxylated surface layer having a positive zeta potential at the adsorption pH.
- "Adsorption pH” is defined as the pH of the water under treatment and for successful operation of the process must be within the range of pH where suspended solids and natural colouring matters in the water retain some of their negative charge.
- the adsorption pH ranges usually from about 3 to about 5 and is most typically the latter. This places some restrictions on the types of water which can be treated and/or renders it necessary to adjust the pH of the water to be treated.
- a method for clarifying water which is hard and/or has a pH in excess of 5 which comprises contacting the water at its natural pH with a coagulant/adsorbent which comprises a finely divided particulate mineral material, the individual particles of which have a thin hydroxylated surface layer having a positive zeta potential at the adsorption pH (as hereinafter defined).
- hard water as used herein has its usual meaning, that is it implies the presence in the water of significant concentrations of calcium and/or magnesium ions.
- the adsorption pH may range from about 5 up to 8.5, or possibly more. Because the presence of calcium and/or magnesium ions in the water to be treated actually enhances the adsorption process, there is no determinable upper limit to the permissible concentration of these ions in the water to be treated. Furthermore, the higher the concentration of calcium and/or magnesium ions in the water to be treated, the higher is the adsorption pH which can be utilized.
- the preferred coagulant/adsorbent is magnetite, preferably having a particle size of less than 10 microns, more preferably 1 to 5 microns.
- the preferred coagulant/adsorbent materials i.e., those typified by magnetite in which the hydroxylated surface layer is derived directly from the substance of the particles, are formed by suspending the particles in an alkali solution for a short period of time, preferably in the presence of air. The particles are then separated from the solution, e.g., by filtration or decantation, and washed with water by the same technique.
- Water treatment is carried out simply by mixing the water to be treated with the coagulant/adsorbent particles, in either a batch or (preferably) continuous process, stirring or agitating the mixture for a period sufficient to allow the suspended (colloidal) impurities and colouring matter in the water to adhere to the particles and separating the particles from the water.
- a polyelectrolyte may be added during the mixing stage, as described in our patent application No. 40032/78.
- the acid wash can be omitted if the pH of the water to be treated with the regenerated adsorbent is 6 or less.
- the present invention includes a method for the regeneration of a loaded coagulant/adsorbent (produced in the above-defined method) which comprises:
- the degree of softness of the water for the various steps will vary according to the pH and hardness of the feed water in the clarification process. Generally, the efficiency of regeneration and the washing steps decreases as the hardness of the water used therein increases but the latter can be as high as 20 ppm of total Ca/Mg without undue detriment. More specifically, using magnetite as the coagulant/adsorbent, it is preferred that the total Ca/Mg in all of the water contacted with the magnetite during regeneration and washing should preferably not exceed 1 meq. per 10 g of magnetite.
- the magnetite particles (10 ml) were added to 200 ml of a sodium hydroxide solution of appropriate concentration (e.g., 0.05N) and stirred for 5 to 10 minutes at 25° C. The particles were then filtered and washed with water.
- a sodium hydroxide solution of appropriate concentration (e.g., 0.05N)
- a 1 l sample of water is contacted with 10 ml of magnetite for 15 minutes at 160 RPM at the optimum pH (determined in prior experiments). The stirring is stopped and the magnetite allowed to settle for 5 minutes. The unfiltered supernatant liquor is then analysed for residual turbidity and colour.
- Clarification was possible at the natural pH, using 1% magnetite with low levels of a number of different polyelectrolytes to reduce turbidity to 0.4 N.T.U. and colour to 3 Pt-Co units.
- regeneration by alkali treatment at pH 10.5 failed to release any turbidity or colour. This shows that hardness helps clarification but hinders regeneration. In this case the hardness was present on the magnetite due to adsorption of Ca 2+ and Mg 2+ ions at pH 7.9 in the clarification stage.
- the magnetite samples were regenerated by alkali treatment at pH 10.5 (i.e., the conditions that previously had failed to achieve turbidity or colour release) and the results are shown in the following table for four magnetite samples which had been used in conjunction with different polyelectrolytes.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AUPE833081 | 1981-04-06 | ||
AUPE8330 | 1981-04-06 |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06567150 Continuation | 1984-01-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
US4882064A true US4882064A (en) | 1989-11-21 |
Family
ID=3769028
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/065,153 Expired - Lifetime US4882064A (en) | 1981-04-06 | 1987-06-19 | Method of removing impurities from hard waters or waters with significant calcium/magnesium concentrations |
Country Status (11)
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5453206A (en) * | 1991-05-27 | 1995-09-26 | Modern Environmental Service Trust | Process for removing silica from aqueous liquors |
US5522992A (en) * | 1991-07-18 | 1996-06-04 | Cervantes; Raul P. | Solution treatment device |
US6099738A (en) * | 1997-12-17 | 2000-08-08 | Micromag Corporation | Method and system for removing solutes from a fluid using magnetically conditioned coagulation |
US20080203015A1 (en) * | 2007-01-09 | 2008-08-28 | Marston Peter G | System and method for enhancing an activated sludge process |
US20100155327A1 (en) * | 2007-01-09 | 2010-06-24 | Steven Woodard | System and method for enhancing a wastewater treatment process |
US8540877B2 (en) | 2007-01-09 | 2013-09-24 | Siemens Water Technologies Llc | Ballasted sequencing batch reactor system and method for treating wastewater |
US8623205B2 (en) | 2007-01-09 | 2014-01-07 | Siemens Water Technologies Llc | Ballasted anaerobic system |
US8840786B2 (en) | 2007-01-09 | 2014-09-23 | Evoqua Water Technologies Llc | System and method for removing dissolved contaminants, particulate contaminants, and oil contaminants from industrial waste water |
US9651523B2 (en) | 2012-09-26 | 2017-05-16 | Evoqua Water Technologies Llc | System for measuring the concentration of magnetic ballast in a slurry |
CN107986494A (zh) * | 2017-12-05 | 2018-05-04 | 云南驰宏锌锗股份有限公司 | 一种脱除铅锌选矿废水中铅离子的方法 |
US10919792B2 (en) | 2012-06-11 | 2021-02-16 | Evoqua Water Technologies Llc | Treatment using fixed film processes and ballasted settling |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1991002698A1 (en) * | 1989-08-16 | 1991-03-07 | Commonwealth Scientific And Industrial Research Organisation | Improved sewage treatment process |
KR950006680B1 (ko) * | 1990-12-07 | 1995-06-21 | 엔비론 움베르트슈츠 아크티엔게젤샤프트 | 정수방법 |
JP2902511B2 (ja) * | 1991-12-24 | 1999-06-07 | 三菱電機株式会社 | 超純水の製造装置、製造方法及び製造装置の制御方法 |
DE4446122A1 (de) * | 1994-12-22 | 1996-06-27 | Sued Chemie Ag | Verfahren zur Herstellung eines Adsorbens für anionische Verbindungen und dessen Verwendung |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3142638A (en) * | 1962-06-29 | 1964-07-28 | Blaisdell Donald Stapf | Process for separating solids from sewage |
US3887498A (en) * | 1973-03-12 | 1975-06-03 | Morton Norwich Products Inc | Method for regeneration of cation exchange resins and for removal of iron deposits therefrom |
US4083782A (en) * | 1973-03-12 | 1978-04-11 | Rohm And Haas Company | Water conditioning process |
US4094778A (en) * | 1977-06-27 | 1978-06-13 | Union Carbide Corporation | Sequestering of CA++ and MG++ in aqueous media using zeolite mixtures |
US4216086A (en) * | 1977-05-27 | 1980-08-05 | Lang John L | Process for clarifying water |
US4279756A (en) * | 1976-05-03 | 1981-07-21 | Commonwealth Scientific And Industrial Research Organization | Water clarification |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1545322A (en) * | 1922-10-28 | 1925-07-07 | Hebden Sugar Process Corp | Regeneration of sugar-purifying reagents |
US2036258A (en) * | 1932-10-05 | 1936-04-07 | Johns Manville | Electropositive composition and method of making the same |
US3233741A (en) * | 1961-06-20 | 1966-02-08 | Johns Manville | Filter aid and method of purifying liquids using the same |
GB1214532A (en) * | 1967-02-16 | 1970-12-02 | Simonacco Ltd | Improvements in or relating to the treatment of aqueous materials |
US3499837A (en) * | 1967-11-20 | 1970-03-10 | Johns Manville | Waste water treatment phosphate removal by iron oxide |
DE2719529A1 (de) * | 1976-05-03 | 1977-11-24 | Commw Scient Ind Res Org | Koagulations- und adsorptionsmittel zur wasserklaerung, unter seiner verwendung durchgefuehrtes wasserklaerungsverfahren und vorrichtung zur durchfuehrung des verfahrens |
GB1563996A (en) * | 1976-08-20 | 1980-04-02 | City University Of St John Str | Method of promoting the sedimentation of clay particles or other negatively charged particles in aqueous suspension |
DE2731939A1 (de) * | 1977-07-14 | 1979-02-01 | Feldmuehle Ag | Verfahren zur reinigung von wasser, insbesondere abwaessern der zellstoff- und papierindustrie |
AU518159B2 (en) * | 1977-09-22 | 1981-09-17 | Commonwealth Scientific And Industrial Research Organisation | use of polyelectrolytes in water clarification |
GB2019378A (en) * | 1978-04-20 | 1979-10-31 | Ici Ltd | Flocculation and removal of organic or inorganic matter from suspensions |
DE2926606A1 (de) * | 1979-07-02 | 1981-01-22 | Henkel Kgaa | Verfahren zur behandlung von abwaessern |
-
1981
- 1981-04-06 AU AU82365/82A patent/AU554857B2/en not_active Expired
-
1982
- 1982-03-31 ZA ZA822230A patent/ZA822230B/xx unknown
- 1982-04-05 GB GB8210076A patent/GB2096126B/en not_active Expired
- 1982-04-05 CA CA000400490A patent/CA1176386A/en not_active Expired
- 1982-04-05 DE DE19823212681 patent/DE3212681A1/de active Granted
- 1982-04-05 NL NL8201445A patent/NL8201445A/nl not_active Application Discontinuation
- 1982-04-06 FR FR8205935A patent/FR2503128B1/fr not_active Expired
- 1982-04-06 JP JP57057961A patent/JPS57177385A/ja active Granted
-
1987
- 1987-06-19 US US07/065,153 patent/US4882064A/en not_active Expired - Lifetime
- 1987-07-30 SG SG616/87A patent/SG61687G/en unknown
- 1987-12-30 MY MY732/87A patent/MY8700732A/xx unknown
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3142638A (en) * | 1962-06-29 | 1964-07-28 | Blaisdell Donald Stapf | Process for separating solids from sewage |
US3887498A (en) * | 1973-03-12 | 1975-06-03 | Morton Norwich Products Inc | Method for regeneration of cation exchange resins and for removal of iron deposits therefrom |
US4083782A (en) * | 1973-03-12 | 1978-04-11 | Rohm And Haas Company | Water conditioning process |
US4279756A (en) * | 1976-05-03 | 1981-07-21 | Commonwealth Scientific And Industrial Research Organization | Water clarification |
US4216086A (en) * | 1977-05-27 | 1980-08-05 | Lang John L | Process for clarifying water |
US4094778A (en) * | 1977-06-27 | 1978-06-13 | Union Carbide Corporation | Sequestering of CA++ and MG++ in aqueous media using zeolite mixtures |
Non-Patent Citations (6)
Title |
---|
Aquatic Chemistry, An Introduction Emphasizing Chemical Equilibria in Natural Waters, Wiley and Sons, p. 478. * |
Environmental Science and Technology, vol. 7, No. 1, Jan. 1973 (Article by S. R. Jenkins entitled Effect of Selected Cation Concentration on Coagulation and Adhesion to Silica Surfaces of ∂--MnO2. |
Environmental Science and Technology, vol. 7, No. 1, Jan. 1973 (Article by S. R. Jenkins entitled Effect of Selected Cation Concentration on Coagulation and Adhesion to Silica Surfaces of MnO 2 . * |
Fine Particles Processing, vol. 1, Proceedings of the International Symposium for Fine Particles Processing, Las Vegas, 1980, published by Amer. Institute of Mining, Metallurgical, and Petroleum Engineers, Inc., 1980. * |
Standard Methods, Hardness, Thirteenth Edition, pp. 178 179, American Public Health Association. * |
Standard Methods, Hardness, Thirteenth Edition, pp. 178-179, American Public Health Association. |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5453206A (en) * | 1991-05-27 | 1995-09-26 | Modern Environmental Service Trust | Process for removing silica from aqueous liquors |
US5522992A (en) * | 1991-07-18 | 1996-06-04 | Cervantes; Raul P. | Solution treatment device |
US6099738A (en) * | 1997-12-17 | 2000-08-08 | Micromag Corporation | Method and system for removing solutes from a fluid using magnetically conditioned coagulation |
US8540877B2 (en) | 2007-01-09 | 2013-09-24 | Siemens Water Technologies Llc | Ballasted sequencing batch reactor system and method for treating wastewater |
US8673142B2 (en) | 2007-01-09 | 2014-03-18 | Siemens Water Technologies Llc | System for enhancing a wastewater treatment process |
US20100155327A1 (en) * | 2007-01-09 | 2010-06-24 | Steven Woodard | System and method for enhancing a wastewater treatment process |
US8470172B2 (en) | 2007-01-09 | 2013-06-25 | Siemens Industry, Inc. | System for enhancing a wastewater treatment process |
US8506800B2 (en) | 2007-01-09 | 2013-08-13 | Siemens Industry, Inc. | System for enhancing a wastewater treatment process |
US20080203015A1 (en) * | 2007-01-09 | 2008-08-28 | Marston Peter G | System and method for enhancing an activated sludge process |
US8623205B2 (en) | 2007-01-09 | 2014-01-07 | Siemens Water Technologies Llc | Ballasted anaerobic system |
US7695623B2 (en) | 2007-01-09 | 2010-04-13 | Cambridge Water Technology, Inc. | System and method for enhancing an activated sludge process |
US8702987B2 (en) | 2007-01-09 | 2014-04-22 | Evoqua Water Technologies Llc | Methods for enhancing a wastewater treatment process |
US8840786B2 (en) | 2007-01-09 | 2014-09-23 | Evoqua Water Technologies Llc | System and method for removing dissolved contaminants, particulate contaminants, and oil contaminants from industrial waste water |
US8845901B2 (en) | 2007-01-09 | 2014-09-30 | Evoqua Water Technologies Llc | Ballasted anaerobic method for treating wastewater |
US10023486B2 (en) | 2007-01-09 | 2018-07-17 | Evoqua Water Technologies Llc | Ballasted sequencing batch reactor system and method for treating wastewater |
US10919792B2 (en) | 2012-06-11 | 2021-02-16 | Evoqua Water Technologies Llc | Treatment using fixed film processes and ballasted settling |
US9651523B2 (en) | 2012-09-26 | 2017-05-16 | Evoqua Water Technologies Llc | System for measuring the concentration of magnetic ballast in a slurry |
CN107986494A (zh) * | 2017-12-05 | 2018-05-04 | 云南驰宏锌锗股份有限公司 | 一种脱除铅锌选矿废水中铅离子的方法 |
Also Published As
Publication number | Publication date |
---|---|
DE3212681C2 (enrdf_load_html_response) | 1991-10-10 |
FR2503128A1 (fr) | 1982-10-08 |
AU8236582A (en) | 1982-10-14 |
DE3212681A1 (de) | 1982-11-25 |
ZA822230B (en) | 1983-02-23 |
NL8201445A (nl) | 1982-11-01 |
GB2096126A (en) | 1982-10-13 |
GB2096126B (en) | 1984-09-05 |
JPS57177385A (en) | 1982-11-01 |
CA1176386A (en) | 1984-10-16 |
JPH0322239B2 (enrdf_load_html_response) | 1991-03-26 |
MY8700732A (en) | 1987-12-31 |
SG61687G (en) | 1987-10-23 |
FR2503128B1 (fr) | 1986-03-07 |
AU554857B2 (en) | 1986-09-04 |
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